FIELD OF THE INVENTION
[0001] The present invention relates to a packing for liquid chromatography, and more specifically,
a packing for liquid chromatography for separation and purification of proteins, enzymes,
nucleic acids, etc. and a process for producing the same.
BACKGROUND OF THE INVENTION
[0002] Generally employed packing materials for liquid chromatography include silica gel,
chemically modified silica gel, synthetic high polymer gels, naturally ocurring high
polymer gels, carbon gel, and the like.
[0003] Hydroxyapatite represented by formula Ca₁₀(PO₄)₆(OH)₂ has been used as a packing
for liquid chromatography for separating high molecular weight biocompounds, such
as proteins, nucleic acids, sugars, glycosides, etc. because of its excellent biocompatibility.
[0004] The hydroxyapatite packing shows both cation exchanging ability and anion exchanging
ability to proteins, etc., while exhibiting high ability in separation of glycosides
in the normal phase mode using acetonitrile and water as a eluent. Owing to such characteristics,
a single column packed with hydroxyapatite can be applied to separation of a variety
of substances. Further, since the desired substance can be separated under mild elution
conditions, the sample under chromatography is protected from deactivation. Furthermore,
the column has a high recovery. Therefore, with developments in the biological industry,
hydroxyapatite has been regarded as one of the most promising packings for chromatography.
That is, hydroxyapatite is the only one of the apatite compound which has hitherto
been used as a packing for liquid chromatography, as described in
Journal of Liquid Chromatography, vol. 9(16), pages 3543 to 3557 (1986).
[0005] However, the hydroxyapatite packing is poor in resistance to dissolution in acidic
solutions, sometimes failing to fulfil its function. That is, when an acidic mobile
phase is passed through a column packed with hydroxyapatite for a long period of time,
crystals of hydroxyapatite are dissolved out, and fine crystals released from the
surface of packing particles and obstruct the passage of the mobile phase, eventually
rendering the packing useless. Therefore, the conventional hydroxyapatite packing
is not suitable for separation processes under acidic conditions. Particularly at
a pH of 5.5 or less, such packing cannot be used continuously, and the range of substances
which can be separated using hydroxyapatite is naturally limited.
[0006] Chlorinated apatite has been reported, as described in "Preparation and Sintering
of Halogen-Bearing Apatite",
Gypsum & Lime, No. 201, pages 89 to 93 (1986). However, its application to chromatography has not
yet been established.
SUMMARY OF THE INVENTION
[0007] An object of this invention is to provide a packing for liquid chromatography having
improved acid resistance while maintaining the advantages of conventional hydroxyapatite
packings, and which exhibits high performance for separating a wide range of substances.
[0008] Other objects and effects of the present invention will be apparent from the following
description.
[0009] The above objects of the present invention have been attained by an apatite packing
for chromatography comprising particles having at least on the surface thereof chlorinated
apatite.
BRIEF DESCRIPTION OF DRAWING
[0010]
Fig. 1A is a chromatogram obtained in Example 1, and Fig. 1B is a chromatogram obtained
in Example 2.
Fig. 2A is a chromatogram obtained in Comparative Example 1, and Fig. 2B is a chromatogram
obtained in Comparative Example 2.
DETAILED DESCRIPTION OF THE INVENTION
[0011] The chlorinated apatite used in the present invenition can be produced by a synthesis
method or an ion exchanging method.
[0012] In the case where the wet method, which is one of the synthesis methods, is employed,
phosphoric acid is added dropwise to a solution containing calcium and chlorine, and
the thus-precipitated solid matter is granulated and pre-calcined to obtain chlorinated
apatite. Calcium and chlorine used herein may be supplied from a single compound such
as calcium chloride, but each may be supplied from separate compounds, respectively.
When calcium and chlorine are supplied separately, calcium hydroxide, calcium acetate,
etc. can be used as a calcium sourse, and hydrochloric acid, ammonium chloride, etc.
can be used as a chlorine sourse.
[0013] In the case where the dry method, which is one of the synthesis methods, is employed,
the chlorinated apatite can be produced according to the method described in "The
Transformation of Choroapatite into Hydroxyapatite",
Indian Journal of Technology, vol.22, pages 301 to 305 (August 1984).
[0014] The wet method can also be conducted according, e.g., to
Ann. Chem. (Paris), vol. 7, 808 to 832 (1952);
J. Res. Nat. Bur. Stand., vol. 72A, 773 (1968); and
Archs. Oral. Biol., vol. 23, 329 to 336 (1978). The dry method can also be conducted according, e.g.,
to
Arch. Intern. Physiol. Biochim., vol. 72, 337 (1964);
Chem. Abstr., vol. 60, 15418a (1964); and
Studii Cercetari Chim., col. 13, 157 (1962).
[0015] In the case of the ion exchanging method, hydroxyapatite particles capable of being
used as a packing for chromatography are immersed in an aqueous solution containing
chloride ions so as to exchange a part of the hydroxyl groups of the hydroxyapatite
for chlorine atoms, and then dried and heat-treated to obtain chlorinated apatite.
Hydrochloric acid is preferably used as the aqueous solution containing chloride ions.
[0016] Examples of the embodiments of the present invention include the following:
(1) a packing comprising chlorinated apatite throughout the individual particles,
(2) a packing comprising apatite particles of which the surface is chlorinated apatite,
and (3) a packing comprising inert carrier particles coated with chlorinated apatite.
[0017] In the above embodiment (1), the whole of the individual particles is formed of the
chlorinated apatite and preferably has a porosity of from 0 to 50% and a specific
surface area of from about 0.01 to 20 m²/g. The porosity can be controlled by changing
the calcining temperature of the density of the particle forming material.
[0018] In the above embodiments (2) and (3), the thickness of the chlorinated apatite surface
layer is preferably about 1µm or more. The porosity and the specific surface area
of the packing are preferably from 0 to 50% and from about 0.01 to 20 m²/g, respectively.
[0019] The above embodiment (1) in which the whole of the individual particles is formed
of chlorinated apatite can be prepared by heat-treating an agglomerate of chlorinated
apatite particles prepared by the above methods at a suitable temperature, as described.
[0020] The above embodiment (2) in which the surface of apatite particles is chlorinated
apatite can be prepared by immersing and stirring an agglomerate of apatite particles
in an aqueous solution containing chloride ions, and then drying and heat-treating
at a suitable temperature, as described.
[0021] The immersing and stirring is generally carried out under acidic conditions at a
temperature of from 5 to 90°C for from 0.5 to 10 hours.
[0022] The above embodiment (3) in which inert carrier particles such as alumina are coated
with chlorinated apatite can be prepared by sputtering or the like methods, as described.
[0023] The packing particles for liquid chromatography of the present invention are not
particularly limited in size, shape, porosity, etc. However, performances such as
separating ability can be assured by following a general particle design for packings
for liquid chromatography. For example, the packing preferably has an average particle
diameter of from about 1 to 100 µm, more particularly from about 10 to 100 µm for
industrial use and from about 1 to 10 µm for use in analyses. If the average particle
size is less than about 1 µm, the pressure drop on passing a liquid sample through
a column packed with the packing becomes too large. If it exceeds about 100 µm, the
surface area of the packing per unit volume is too small to assure separating ability.
The packing preferably has a shape near to a spherical form in order to obtain stable
separation characteristics while preventing cracks or cutouts, although particles
having a macadamized form may be used. The porosity is preferably high in view of
the load of the samples, but non-porous packing may be used, for example, for analytical
purposes. The specific surface area is preferably from about 0.01 to 20 m²/g, although
it may be varied depending on the form of the packing particles.
[0024] The packing of the present invention can be used for a method for liquid chromatography
by sequentially (a) packing a column with the packing of the present invention, (b)
contacting the packing with a sample comprising at least one solute, and (c) contacting
the packing with a liquid mobile phase to separate the solute by elution.
[0025] Upon carrying out the method for liquid chromatography, the preferred eluents are
as follows: In an ion exchanging mode, (1) a sodium phosphate buffer (pH 5 to 9),
(2) a potassium phosphate buffer, (3) a mixture of a sodium chloride solution and
various buffers (e.g., tris buffer, pipes buffer, etc.) and (4) a mixture of a potassium
chloride solution and varous buffers (e.g., tris buffer, pipes buffer, etc.). In the
cases of (1) and (2), a gradient elution at a concentration of from 10-100 mM to 1
M is preferred. In a normal mode, an isocratactic elution with the acetonitrile/water
ratio of from about 7/3 to 9/1, and a gradient elution while increasing the water
concentration are preferred.
[0026] The packing for liquid chromatography according to the present invention can be suitably
applied to separation of solutes such as proteins (e.g., monoclonal antibody and fibronectin),
enzymes (e.g., ligase and protease), nucleic acids, (e.g., nucleotide, oligonucleotide,
DNA and RNA), glycosides (ginsenoside, steviside, rebaudioside and saponin), and so
on and exhibits stable separation performance even in an acidic solution, e.g., phosphoric
acid, hydrochloric acid, etc. having pH of 3 or more.
[0027] The present invention is now illustrated in greater detail with reference to the
following Example and Comparative Example, but the present invenition is not to be
construed as being limited thereto.
[0028] Unless otherwise indicated, all parts, percents, ratios and the like are by weight.
EXAMPLE 1
[0029] 8 g of spherical apatite particles were added to an aqueous solution of hydrochloric
acid having a pH of 4.5. The mixture was reacted for 1 hour while stirring, and after
filtering and drying by evaporation, the particles were heat-treated to obtain a powderous
packing. The formation of chlorinated apatite by the above procedures was confirmed
by X-ray diffractiometry, infrared absorption, etc.
[0030] The thus-obtained packing was filled in a stainless steel column having a diameter
of 7.5 mm and a height of 100 mm. A sample solution containing a phosphoric acid buffer
solution (pH=6.8) having dissolved therein 10 µg/µℓ of bovine serum albumin, 1.25
µg/µℓ of lysozyme, and 5 µg/µℓ of cytochrome C was passed through the column.
[0031] Elution was made by a linear gradient method at a flow rate of 1.0 mℓ/min for 30
minutes by using a sodium phosphate buffer (pH=6.8) having a concentration of from
0.01 to 0.4M as an eluent so as to obtain the chromatogram shown in Fig. 1A.
[0032] In Figs. 1A, 1B, 2A and 2B, peak 1 is the peak of bovine serum albumin, peak 2 is
the peak of lysozyme, and peak 3 is the peak of cytochrome C.
EXAMPLE 2
[0033] After passing through a column filled with the packing prepared in Example 1 a sodium
phosphate buffer having a pH of 5.0 and a concentration of 0.4M at a flow rate of
1.0 mℓ/min for 10 hours, the sample solution used in Example 1 was separated in the
same manner as in Example 1 so as to obtain a chromatogram shown in Fig. 1B.
[0034] As is clear from Figs. 1A and 1B, when the chlorinated apatite packing according
to the present invention was used, no peak splitting occured even after a 0.4M sodium
phosphate buffer having a pH of 5.0 was passed for 10 hours. Thus, stable high separation
performance was attained over a long period.
COMPARATIVE EXAMPLE 1
[0035] The same procedures as in Example 1 were repeated except that a conventional hydroxyapatite
packing was used instead of the packing of the present invention used in Example 1
so as to obtain the chromatogram shown in Fig. 2A.
COMPARATIVE EXAMPLE 2
[0036] After passing through the column a 0.4M sodium phosphate buffer having a pH of 5.0
for 10 hours, the same procedures as in Comparative Example 1 were repeated so as
to obtain a chromatogram shown in Fig. 2B.
[0037] As is clear from Figs. 2A and 2B, when the conventional hydroxyapatite packing was
used, peak splitting caused by the deterioration of the column occured after a 0.4M
sodium phosphate buffer having a pH of 5.0 was passed for 10 hours.
[0038] As described above, the packing for liquid chromatography according to the present
invention has excellent acid resistance while maintaining high separation performance
of conventional hydroxyapatite packings, and does not deteriorate even after passing
an acidic solution therethrough over a long period. Therefore, the packing of the
present invention can be used stably for separating various compounds, particularly
proteins, enzymes, nucleic acids, sugar, glycosides, etc., even in an acidic region
for a long period of time.
[0039] While the invention has been described in detail and with reference to specific embodiments
thereof, it will be apparent to one skilled in the art that various changes and modifications
can be made therein without departing from the spirit and scope thereof.
1. An apatite packing for liquid chromatography comprising particles having at least
on the surface thereof chlorinated apatite.
2. An apatite packing for liquid chromatography as claimed in claim 1 wherein the
average diameter of said packing particles are from 1 to 100 µm.
3. An apatite packing for liquid chromatography as claimed in claim 1, wherein the
whole of the particles of said packing is formed of said chlorinated apatite.
4. An apatite packing for liquid chromatography as claimed in claim 1, wherein said
packing comprises apatite particles having on the surface thereof said chlorinated
apatite.
5. A method for producing an apatite packing for liquid chromatography comprising
the step of: immersing and stirring an agglomerate of apatite particles in an aqueous
solution containing chloride ions so as to convert said apatite particles into chlorinated
apatite.
6. A method for producing an apatite packing for liquid chromatography as claimed
in claim 5, wherein said immersing and stirring step were carried out at a temperature
of from 0.5 to 90°C for from 0.5 to 10 hours.
7. A method for liquid chromatography comprising the steps of:
(a) packing a column with an apatite packing comprising chlorinated apatite;
(b) contacting said packing with a sample comprising at least one solute;
(c) contacting said packing with a liquid mobile phase to separate said solute by
elution.
8. A method for liquid chromatography as claimed in claim 7, wherein said solute is
selected from a protein, an enzyme, a nucleic acid and a glycoside.
9. A method for liquid chromatography as claimed in claim 7, wherein said mehtod for
liquid chromatography is conducted at a pH of 3 or more.